System and method for treating asbestos

ABSTRACT

A method, apparatus, and system to apply a mineralizing agent to an asbestos containing material (ACM) after the ACM is reduced in size, particularly by spraying or injecting the mineralizing agent to a shredded ACM, is provided. The mineralizing agent may include a solution of alkali metal hydroxide, alkali metal silicate, alkali metal borate, alkaline earth borate, or mixtures thereof, which may be heated and mixed and is then delivered to the reduced size or shredded ACM using a piping system that injects the mineralizing agent downstream of an ACM shredding unit. The ACM treated with the mineralizing agent may be heated in a mineralizing furnace to convert the ACM to an essentially asbestos-free mineral. After removal from the mineralizing furnace, the mineralized material is moved to an atmosphere controlled environment where it is cooled gradually for further mineralization.

CROSS REFERENCE TO RELATED APPLICATIONS

This application is a continuation of U.S. application Ser. No.12/243,805, which is a continuation in part of U.S. application Ser. No.11/994,072, which entered the National Stage under 35 USC 371 fromInternational Application No. PCT/US2006/026018 for a “System and Methodfor Accelerating the Conversion of Asbestos in the Process ofMineralogical Conversion,” filed by the applicant herein and having aninternational filing date of Jun. 30, 2006, as amended on Dec. 27, 2007.

BACKGROUND

1. Technical Field

The present disclosure relates to the treatment of asbestos containingmaterial (ACM) with a mineralizing agent using a method, system, andapparatus that increases the receptivity of the ACM to the mineralizingagent.

2. Description of the Related Art

Asbestos is a term referring to a family of historically useful fibrousminerals that most commonly belong to the serpentine and amphibolemineral groups including such species as chrysotile, crocidolite,amosite, and anthophyllite. More precisely referred to as “asbestiformminerals,” they are hydrated silicates that generally containsubstituted iron, calcium, magnesium, and sodium in various proportions.The serpentine group of minerals that includes chrysotile, antigorite,and lizardite are all represented by the approximate composition: Mg₃[Si₂ O₅] (OH)₄. Of these, chrysotile represents the majority of allasbestos minerals used for industrial and commercial purposes. There issubstantial variation in mineral chemistry and physical characteristicsof asbestiform minerals, but they all have similarities in basicstructure that are typically modified because of variations in theconcentrations of calcium, iron, magnesium, and sodium.

Asbestos has been used in thousands of products and in numerousworkplaces. Although the harm caused by asbestos is not apparent atfirst, asbestos exposure can lead to serious, debilitating, and oftenfatal diseases. These include mesothelioma, asbestos lung cancer, andasbestosis. Usually, a period of 10 to 40 years or more passes beforethe asbestos victim exhibits the first asbestos disease symptoms. In theworkplace, there is no “safe” level of asbestos exposure. For thisreason, increased limitations and restrictions on asbestos use incommercial products, handling, and disposal have been and continue to beimposed in many countries around the world.

As a toxic mineral, various attempts have been made to render asbestosinert so that it can be safely handled and disposed. Attempts to destroyasbestos waste using heat alone to alter asbestos fiber chemistry havemet with only limited success since asbestos fibers by their very natureare refractory and self-insulating. For example, chrysotile fibers havebeen reported to withstand temperatures up to 3000° F. for time periodsof up to one-half hour. Since such a technique requires very hightemperatures for fiber destruction, this approach has proved quiteuneconomical.

Several vitrification (or melting) processes, such as plasma melting andjoule heating, have shown success in destroying asbestiform minerals.However, these processes are energy intensive and require very expensiveand complex equipment. Thus, vitrification processes, although capableof destroying asbestos waste, have not exhibited commercial viability.

Other methods that utilize reduced process temperatures and a variety ofchemical additives have also been attempted. With one exception, theyhave also met with limited success. The process of “MineralogicalConversion of Asbestos Waste” described in U.S. Pat. No. 5,096,692,which is incorporated by reference in its entirety herein, is the onesub-melting point process that has achieved commercial development. Inthat patent, asbestos waste is converted to non-asbestos products belowthe melting point by the combination of chemical additives and theapplication of heat.

During the commercial development of Mineralogical Conversion ofAsbestos Waste, it was found that the time required to convert 100% ofthe asbestos fibers in the waste took longer than that which would berequired for other competitive though less efficient processing methods.Processing times of up to 60 minutes were required to assure that all ofthe asbestos fibers in the waste experienced destruction. The processingtime was substantially reduced by the System and Method for Acceleratingthe Conversion in Asbestos in the Process of Mineralogical Conversioncovered by Patent Cooperation Treaty Application No. PCT/US2006/026018,which is incorporated by reference in its entirety herein, wherein theasbestos containing materials are broken or shredded into particles, theparticles are treated with a mineralizing agent, and the particles areheated in a furnace. It is desirable to further reduce the processingtime in order to enhance the commercial viability of this process forlarge scale commercial applications.

BRIEF SUMMARY

Mineralization of asbestos containing materials (ACM) can be acceleratedand made more efficient when a mineralizing agent is applied after theACM is shredded. In particular, it has been discovered by the inventorthat application of the mineralizing agent to shredded ACM at acontrolled rate in accordance with the amount of ACM shredded, such asby weighing or measuring the amount of ACM before or after shredding,reduces the amount of mineralizing agent required, reduces the timerequired for mineralization, and increases the conversion rate of ACMinto non-asbestos materials containing non-detectable concentrations ofasbestos when analyzed using transmission electron microscopy, X-raydiffraction, and optical microscopy techniques.

In accordance with one embodiment, an apparatus that treats the ACM isprovided. The apparatus includes a shredding system adapted to receiveand shred the ACM into a shredded ACM; a chamber situated in theshredding system to receive the shredded ACM; and a delivery systemadapted to deliver a mineralizing agent to the shredded ACM within thechamber. In one form the apparatus includes one or more storage areas tostore the ACM, a transport mechanism to move the ACM, and a hopper thatreceives the moved ACM. The ACM may be in either bagged or unbaggedform.

In accordance with another embodiment, a mineralizing agent deliverysystem is provided that includes a spray apparatus adapted to deliverthe mineralizing agent to the shredded ACM. Ideally, the spray apparatusincludes a device to control the amount of the mineralizing agentsprayed onto the shredded ACM based on the weight of the shredded ACM.In one embodiment, the spray apparatus is equipped with components toprepare the mineralizing agent for application to the shredded ACMincluding a unit adapted for the addition of a concentrated alkali metalhydroxide, a concentrated alkali metal silicate, a concentrated alkalinemetal borate, or mixtures thereof to a tank; a mixer to add and mixwater and the concentrated mineralizing agent in the tank; a unit tomeasure and control the mineralizing agent's concentration; a system totransfer the mineralizing agent to a day tank for supply and applicationto the shredded ACM; a system to measure and control the rate at whichthe mineralizing agent is applied to the shredded asbestos wastecommensurate with the weight of asbestos being fluxed; and a flushsystem for cleaning, testing, and draining of the tank and associatedequipment and systems. The tank and associated equipment and systems mayor may not be heated, insulated, or heat traced.

Another embodiment of the apparatus or system includes a mineralizingagent addition container, a mineralizing agent transfer mechanism tomove the mineralizing agent from the mineralizing agent additioncontainer to a mix tank, a mix tank equipped with a water additiondevice, a mixer to mix the mineralizing agent and the water in the mixtank, a heater to heat the mineralizing agent, transfer andrecirculation lines to move the mixed mineralizing agent solution to aheated day tank for storage before application of the mineralizing agentto the shredded ACM, and a mineralizing agent application system adaptedto apply the mineralizing agent such as a borax solution to the shreddedACM. In one preferred embodiment, the mineralizing agent applicationsystem is adapted to spray the mineralizing agent onto the shredded ACMusing a supply line, a spray header, spray nozzles, a timed orvolume-controlled valve for application of the mineralizing agent, andthe associated piping, valves, sensors, pumps, and other equipment thatwill be appreciated by those skilled in the art with fluid supplysystems to transport the mineralizing agent for application to theshredded ACM. All of the before stated equipment may be heated, heattraced, or insulated.

In another embodiment, the apparatus or system may be modified to beequipped with an addition container for the addition of a concentratedborax solution. Alternatively, the apparatus or system may be modifiedto include an addition container for the addition of a concentratedalkali metal hydroxide, a concentrated alkali metal silicate, aconcentrated alkaline metal borate, or mixtures thereof.

In accordance with another embodiment, the shredding system is adaptedto include a shredding device that shreds the ACM, an exit portal fromthe shredding device that discharges the shredded ACM by the combinedforce of gravity and the force exerted by the force of the shreddercutters, and a conveyor, mixer, or agitator that maintains the shreddedACM in a suspended, mixed, or dispersed form for receipt of themineralizing agent. The shredding device may be of any commerciallysuitable type. In a preferred embodiment, the shredding device is a slowspeed rip-shear shredder, however, it may also be a crosscut shredderwith a capacity to shred the ACM at a rate consistent with theprocessing capacity of the mineralizing furnace.

In a further preferred embodiment, the mineralizing agent applicationsystem is adapted to distribute the mineralizing agent over the shreddedACM as it exits the shredding device's exit portal. The mineralizingagent application system may be equipped with nozzles, sprayers, orother methods for efficient distribution of mineralizing agent to themaximum surface area of shredded ACM. In one embodiment, instrumentationis supplied to measure the weight of the ACM, either before or aftershredding and in bagged or unbagged form. Further instrumentation,equipment, and controls may be provided to apply the mineralizing agentin accordance with the weight of the shredded ACM.

In accordance with another embodiment, the process by which ACM istreated with a mineralizing agent includes delivering the raw ACM,either in plastic bags or in free form, onto a conveyor or othertransfer device; delivering the raw ACM to a shredder that shreds theraw ACM, including any plastic bags, or associated debris and the ACMtherein (collectively shredded ACM); and applying the mineralizing agentto the shredded ACM using a mineralizing agent delivery system. In apreferred embodiment, the mineralizing agent delivery system applies themineralizing agent to the shredded ACM in a spray form. In anotherembodiment, the amount of mineralizing agent applied to the shredded ACMis metered based upon the weight of the shredded ACM.

In accordance with at least one further embodiment, the mineralizingagent is applied using a mineralizing agent delivery system and methodthat includes adding a concentrated mineralizing agent to a mix tank,measuring the amount of the concentrated mineralizing agent added to themix tank, adding water to the concentrated mineralizing agent in the mixtank to make the mineralizing agent, measuring the concentration andvolume of the mineralizing agent, transferring the mineralizing agent toa day tank, and transporting the mineralizing agent from the day tank tothe delivery system through which the mineralizing agent is applied tothe shredded ACM. The mix tank, day tank, and delivery system may beconnected by a system of pumps, pipes, valves, meters, sensors,thermocouples, thermometers, regulators, and other related componentstypically used in fluid transfer systems, some or all of which isheated, insulated, or heat traced. In a preferred embodiment, themineralizing agent is a solution of an alkali metal hydroxide, asolution of an alkali metal silicate, a solution of an alkaline metalborate, or any combination thereof.

In another embodiment, a method or process for applying the mineralizingagent is provided. The method includes mixing water with an alkali metalhydroxide solution, an alkali metal silicate solution, an alkaline metalborate solution, or mixtures thereof in a mix tank to make themineralizing agent; using a mixer in the mix tank to mix the water withthe mineralizing agent to make a mineralizing agent having aconcentration in the range of about 8 and 12 percent by weight of analkali metal hydroxide solution, an alkali metal silicate solution,alkaline metal borate solution, or mixtures thereof. In one embodimentthe concentration of the mineralizing agent is measured and themineralizing agent is applied to the shredded ACM through nozzles at ameasured rate based upon the amount of the shredded ACM. Alternatively,the mineralizing agent is applied as the ACM is in the process of beingshredded.

In accordance with another embodiment, after the shredded ACM is treatedwith the mineralization agent, it may be further processed formineralization, most preferably as described in InternationalApplication No. PCT/US2006/026018, which includes using a heatingmineralization process. The inventor has discovered that themineralization conversion rate to non-asbestos containing mineralsincreases if the particles that exit the mineralizing furnace or kilnare allowed to cool gradually in an atmosphere controlled unit orcontainer. Alternatively, the residence time in a mineralization furnaceis reduced when the heated particles are allowed to cool gradually in anatmosphere controlled area upon exiting the mineralizing furnace.

In accordance with another embodiment, the process of mineralizing ACMis improved by the transport of the particles removed from amineralizing furnace or kiln to an atmosphere controlled unit forgradual cooling. The resultant product is a non-asbestos mineralcontaining non-detectable concentrations of asbestos when analyzed usingtransmission electron microscopy, X-ray diffraction, or opticalmicroscopy techniques. Energy savings of between about 400,000 BTU perton and 600,000 BTU per ton of the processed ACM are realized bygradually cooling the ACM particles in an enclosed atmosphere controlledarea.

BRIEF DESCRIPTION OF THE SEVERAL VIEWS OF THE DRAWINGS

The foregoing and other features and advantages of the presentdisclosure will be more readily appreciated as the same become betterunderstood from the following detailed description when taken inconjunction with the following drawings.

In the drawings identical reference numbers identify similar elements oracts. The sizes and relative positions of elements in the drawings donot necessarily indicate locations and are not necessarily drawn toscale. Some elements are enlarged to improve legibility and for ease ofdescription. Further, the particular shape of elements as drawn are notintended to convey any information regarding the particular shape of theactual elements, and have only been selected for ease of recognition.

FIG. 1 is a schematic diagram of the method disclosed in PCT ApplicationNo. US2006/026018;

FIG. 2 is a schematic of one embodiment of a system and method fortreating asbestos with a mineralizing agent after asbestos containingmaterial (ACM) is shredded in accordance with the present disclosure;and

FIG. 3 is an enlarged cross-sectional side view of a nozzle formed inaccordance with the present disclosure.

DETAILED DESCRIPTION

In the following description, one skilled in the relevant art willrecognize that embodiments may be practiced without one or more of thespecific details described in the specification, or with other methods,components, materials, etc. In other instances, well-known structureshave not been shown or described in detail to avoid unnecessarilyobscuring descriptions of the embodiments.

Unless the context requires otherwise, throughout the specification andclaims that follow, the word “comprise” and variations thereof, such as,“comprises,” “comprising,” “including,” and variations thereof, such as“included,” are to be construed in an open, inclusive sense, that is as“including, but not limited to.”

References throughout this specification to “one embodiment” or “anembodiment” means that a particular feature, structure or characteristicdescribed in connection with the embodiment is included in at least oneembodiment. Thus, the appearance of the phrases “in one embodiment” or“in an embodiment” in various places throughout this specification arenot necessarily all referring to the same embodiment. Furthermore, theparticular features, structures, or characteristics may be combined inany suitable manner in one or more embodiments.

As used in this specification and the appended claims, the singularforms “a,” “an,” and “the” include plural referents unless the contextclearly indicates otherwise. It should also be noted that the term “or”is generally employed in its sense that includes “and/or” unless thecontext clearly dictates otherwise.

For purposes of clarity and ease of comprehension, directional termssuch as upstream and downstream may be used to indicate a sequence butare not intended to limit the scope of the invention. For ease ofreference and for descriptive purposes, the processing environment ofPCT Application No. US2006/026018, “System and Method for Acceleratingthe Conversion of Asbestos in the Process of Mineralogical Conversion”may be used, but should not be interpreted as limiting.

Asbestos is a naturally occurring mineral that has historically beenused for many commercial, building, construction, and residentialpurposes. Asbestos minerals are generally classified as any asbestosmineral fibers, including the minerals chrysotile, amosite,anthophyllite, crocidolite, but can include other mineral complexes, inparticular, mixtures of asbestos mineral fibers with additive or matrixsubstances including inorganic and organic materials. When removed fromcommercial, building, construction, and residential sites, thesematerials are often mixed with cement, gypsum, plaster, dolomite, and avariety of silicates or other building materials. Typically, thiscomposite of materials have been broken into manageable pieces andplaced in plastic bags (collectively referred to as ACM).

Once the ACM is removed from an installation site, it is subsequentlytransported to a processing or disposal facility. As described in theabove referenced International Application No. PCT/US2006/026018, oneprocess for treating ACM is mineralogical conversion. Mineralogicalconversion can be accomplished using a mineralizing agent and heatingthe ACM in a mineralizing furnace, thereby converting the ACM into anasbestos free mineral containing non-detectable concentrations ofasbestos when analyzed using transmission electron microscopy, X-raydiffraction, and optical microscopy techniques.

Generally and in accordance with one embodiment, the method includesapplying a mineralizing agent in spray form after the ACM is shredded toreduce the time required for mineralization in a mineralizing furnacefrom about 30 minutes down to about 20 minutes and to reduce the energyusage of the mineralizing furnace associated with reduced mineralizationtime and the reduced introduction of liquid mineralizing agent to thefurnace. Typical energy savings are between about 1,000,000 btu per hourat shredded ACM processing rates of 2000 pounds per hour for shreddedACM having particle diameters of between about 1 inch to and including 2inches and a density between about 15 pounds per cubic foot and 50pounds per cubic foot.

In accordance with various embodiments, the problem of ineffective andinefficient application of the mineralizing agent to the ACM is solvedby decreasing the size of the ACM. The method for decreasing the size ofthe ACM includes processing the container holding the ACM, such asplastic bags (collectively referred to as ACM) into shredded ACM;preparing a mineralizing agent for application to the shredded ACM; andapplying the prepared mineralizing agent to the shredded ACM. The rateat which the mineralizing agent is applied to the shredded ACM may be ata controlled rate and may be performed in a manner that evenlydistributes the mineralizing agent over the shredded ACM.

The raw ACM, whether in a plastic bag or not, may be reduced in size bya shredding system that shreds the ACM to a particle diameter sufficientto pass through a screen possessing 2 inch openings. The mineralizingagent is applied in spray form to the shredded ACM. In one embodiment,the amount of mineralizing agent applied is controlled in accordancewith the weight of the ACM fed to the shredding system. In yet anotherembodiment, the raw bagged or unbagged ACM is first weighed or measuredto determine the amount of mineralizing agent to be applied thereto.Alternatively, a partial vacuum is induced by one or more blowers on theentire system that creates or handles shredded ACM to prevent release ofasbestos fibers, and the blower air is passed through a high-efficiencyfilter to capture fibers that may have been drawn out of the processingsystem.

A method is also provided that includes preparing a solution of themineralizing agent for application to the shredded or reduced-size ACM.This includes using a mix tank wherein water is mixed with aconcentrated mineralizing agent that may include an alkali metalhydroxide, an alkali metal silicate, an alkaline metal borate, ormixtures thereof; using a mixer in the mix tank to formulate amineralizing agent having a concentration in the range of about 8 and 12percent by weight of an alkali metal hydroxide, an alkali metalsilicate, an alkaline metal borate, or mixtures thereof and measuringand controlling the mineralizing agent's concentration; transferring themineralizing agent to a day tank for supply and application to thereduced size or shredded ACM; using an insulated or heat traced supply,transfer, and recirculation lines that connect the mix tank, the daytank, and the unit at which the mineralizing agent is applied to thereduced size or shredded ACM; and then using a mineralizing agent sprayapparatus which may include valves and controllers, to regulate theamount of the mineralizing agent applied based on the amount of thereduced size or shredded ACM.

In a preferred embodiment, the mineralizing agent spray apparatus isequipped with nozzles to spray the mineralizing agent onto the shreddedACM. The spray nozzles, which may be inserted into the asbestosshredding system downstream of a shredder or shredding unit, deliver themineralizing agent to the shredded ACM while the shredded ACM issuspended, agitated, or mixed. The spray nozzles may be one nozzle, aseries of nozzles, or a plurality of nozzles that apply the mineralizingagent in unison, in series, or in stages. In one embodiment, the spraynozzles are situated to apply the mineralizing agent to the shredded ACMas the shredded ACM exits the shredding system or shredder.

The mineralizing agent is heated by a system that stores themineralizing agent in a temperature controlled tank, mix tank, orvessel. The tank, mix tank, or vessel may be insulated or heat traced tomaintain the mineralizing agent at an elevated temperature. Mostpreferably, the mineralizing agent will be maintained at a temperaturein the range of about 120 degrees Fahrenheit and 160 degrees Fahrenheit.The associated pumps, piping, valves, controllers, and other equipmentused by those skilled in the art for such mixing and transfer systemsmay also be heated, insulated, or heat traced.

After the shredded ACM is treated with the mineralizing agent, it canproceed to further mineralizing processes, which includes processing ina mineralizing furnace or kiln for mineralization of the ACM to anessentially non-asbestos containing mineral. Ideally, after the ACM ismade into a shredded ACM, the mineralizing agent is applied, theshredded ACM is compacted into compacted particles, the compactedparticles are broken up into particles, and the particles are spread ina furnace where they are heated and mineralized to an asbestos-freemineral.

The inventor has found that conversion to the asbestos-free materialafter removal from a mineralizing furnace or kiln continues for a shorttime if the hot treated ACM is allowed to gradually cool upon exitingthe mineralizing furnace in an atmosphere controlled unit. The resultantproduct is an asbestos-free material containing non-detectableconcentrations of asbestos when analyzed using transmission electronmicroscopy, X-ray diffraction, and optical microscopy techniques. Thetime required for heating in the mineralization furnace can be reducedby about between 1 minute and 2 minutes using a method of graduallycooling the particles that exit the mineralizing furnace in anatmosphere controlled unit for gradual cooling and furthermineralization. The expected energy savings are in the range of about200,000 BTU's and 400,000 BTU's per ton of shredded ACM processed.

In accordance with another embodiment, the method of cooling theparticles that exit the mineralization furnace or kiln includestransferring the particles exiting the mineralization furnace or kiln toan atmosphere controlled unit and gradually cooling the particles.

In accordance with another embodiment, the method includes operatingunder approximately 0.5 inches of water of vacuum in an enclosedenvironment in which filters collect particulates to prevent emissionsof asbestos or ACM during treatment of the ACM, including shredding andall transfer operations of the ACM, the shredded ACM, and the compressedACM and ACM particles.

A system is also provided that treats ACM with a mineralizing agent toconvert the asbestos into asbestos-free minerals using a unit totransfer ACM, either bagged in plastic or other types of material orunbagged (bags and ACM collectively referred to as ACM) to a device thatreduces the size of the ACM particles to make a reduced size ACM; adevice that treats the reduced size ACM particles with the mineralizingagent thereby yielding a treated ACM; a compaction unit that compressesthe treated ACM into a compressed ACM; a unit that transfers thecompressed ACM into the mineralizing furnace; a unit that breaks up thecompressed ACM into broken-up particles inside the mineralizing furnace;a unit that spreads the broken-up particles in a mineralizing furnace; aheat source that applies heat directly to the broken-up particles; and asystem that cools the heated broken-up particles in an atmospherecontrolled chamber.

The device that reduces the size of the ACM particles is preferably ashredder to make shredded ACM. Other embodiments may use one or moreother devices that tear the ACM to increase the surface area availableto receive the mineralizing agent. The ACM particles may be shredded,torn, or otherwise reduced in size to receive the mineralizing agentusing a shredder, grinder, crusher, or other device capable of reducingthe size of the ACM particles to a size optimal for reception of themineralizing agent.

Another feature includes a mixer, an agitator, or another unit capableof distributing the reduced size ACM in a chamber so that the reducedsize ACM surface area is maximized for reception of the mineralizingagent.

The device that treats the reduced size ACM with the mineralizing agentincludes a mix tank wherein water and the mineralizing agent is mixed; aday tank to store the mineralizing agent prior to applying themineralizing agent to the reduced size ACM or the shredded ACM; a devicethat measures the concentration and volume of the mixed water and themineralizing agent (collectively called mineralizing agent); a transfermechanism to transport the mineralizing agent between the mix tank, daytank, and a mineralizing agent application apparatus that appliesmineralizing agent to the shredded ACM.

In accordance with a further embodiment, the mineralizing agentapplication apparatus includes an injection system, spray nozzle, orother injectors that evenly disperse the mineralizing agent over thereduced size ACM or the shredded ACM. The mineralizing agent applicationapparatus includes pumps, pipes, valves, meters, sensors, regulators,instruments, and other related components that will be appreciated bythose skilled in the art of fluid transfer systems. In a preferredembodiment, the components of the mineralizing agent application systemare heated, heat traced, or insulated.

The system transfers material that exits a mineralizing heater or kilnto a controlled-atmosphere area where the materials cool gradually. Aunit is provided that moves the ACM, the reduced size ACM, the shreddedACM, the compressed ACM, the broken-up particles, and the resultantessentially asbestos-free minerals while hot.

In accordance with another aspect of the present disclosure, the systemincludes an assembly that encloses the ACM, the shredded ACM, the brokenup particles, the compressed ACM, and the particles, and collectsparticulates, dust and other emissions using a filtration apparatus. Ina preferred embodiment, a device is provided that applies a vacuum ofapproximately 0.5 inches of water to prevent emissions.

Referring to FIG. 1, mineralogical conversion is accomplished by aconversion system 10 in which ACM 12 is introduced into a shreddingsystem 14 wherein the ACM is reduced in size for rapid acceptance and/orabsorption of the mineralizing agent. The size-reduced ACM 16 passesinto a housing and mixer 18 and enters a compaction device 20 thatcompresses the ACM to a minimum density in the range of about 15 to 50pounds per cubic foot and discharges the compressed ACM 22. Thecompressed ACM 22 is discharged to a mineralizing furnace 24 where theACM 22 is heated 26 and encounters a granulating shaft 28 or a series ofgranulating shafts to reduce the heated ACM into smaller compacted ACMparticles 30. The ACM particles 30 then are moved to astirring/spreading shaft 32 that spreads the smaller compacted ACMparticles 34 in the furnace 24. A heat source 36 is located in thefurnace 24 downstream of the stirring/spreading shaft 32, and it appliesheat directly to the spread ACM particles 34. A resultant asbestos freemineral 38 is generated, which is discharged into a transport device 40for removal to a storage container 41.

The inventor has discovered that mineralogical conversion of ACMproceeds more rapidly and more efficiently by applying a mineralizingagent to the ACM evenly after the ACM is reduced in size. Shown in FIGS.1 and 2 is one embodiment of the present disclosure in which the ACM 12is delivered to the shredding system 14 where the ACM is shredded and amineralizing agent 42 is distributed to mineralizing agent nozzles 44using mineralizing agent application header 46, thereby resulting intreated ACM 17. An injection system (described below) applies themineralizing agent 42 in a spray, mist, atomized, droplet, or otherhighly dispersed form, preferably while the shredded or reduced size ACM16 is suspended, spread, or mixed. In one embodiment, the shredded ACMis discharged through a screen 80 by propulsion of the shredding system14 and gravity, thereby distributing the shredded ACM for reception ofthe mineralizing agent. The spray or injection nozzles 44 can beobtained from several commercially available sources and will not bedescribed in detail herein. Briefly, the configuration shown in FIGS. 2and 3 is intended to keep the nozzles 44 hot to prevent crystallizationof the solution. They are configured to automatically drain by gravitybetween applications or in the event of process interruption to preventcrystallization. If crystallization occurs, the nozzles 44 will becomeobstructed.

As shown in FIG. 2, the mineralizing agent 42 is injected into a chamberhousing and mixer 18 downstream of the shredding system 14 throughinjection ports 48 in the nozzles 44. Referring to FIG. 2, themineralizing agent 42 is prepared by using an addition container 50 anda transfer mechanism or conduit 52, a mix tank 54, a day tank 56, aplurality of pumps 58, supply and recirculation lines 60, a mineralizingagent application header 46, an injection port 48 or a plurality ofspray nozzles 44, and a timed or volume-controlled valve 62 to controlthe rate of the addition of the mineralizing agent 42 to the header 46.The mix tank 54 is in fluid communication with the day tank 56, thesupply and recirculation lines 60, the mineralizing agent applicationheader 46, the spray nozzles 44, and the timed valve 62 by a system ofpipes, valves, controllers, meters, instrumentation, and other equipmentrecognized in the art as suitable for use in the transfer of fluids. Inone embodiment, the mix tank 54, day tank 56, transfer and recirculationlines 60, mineralizing application header 46, and injection nozzles 44may be heated or insulated 47 in a conventional manner.

A concentrated borax solution is preferably used as the mineralizingagent 42 that is mixed with water. However, the mineralizing agent 42may be a solution of an alkali metal hydroxide, an alkali metalsilicate, an alkaline metal borate, or any combination thereof. Inanother embodiment, the mix tank 54 is equipped with a mixer 64, and themix tank 54, the addition container 50, a transfer mechanism 52, a daytank 56, a plurality of pumps 58, supply and recirculation lines 60, amineralizing agent application header 46, an injection port or aplurality of spray nozzles 44, and a timed or volume-controlled valve 62to control the rate of the addition of the mineralizing agent areconnected to and controlled by an instrumentation system 66 to monitorand control the mixing, concentration, management, circulation, anddistribution of the mineralizing agent. The mixed borax solution istransferred to the heated, insulated day tank 56 before it is deliveredto the shredder 14. The transfer system includes insulated, heat-traced,recirculation lines 60 and a plurality of pumps 58 to allow circulationand flushing of the system to prevent plugging.

The heated, mixed borax solution 42 is delivered from the day tank 56through the recirculation lines 60 and header 46 to the shredded ACM 16,most preferably through the spray system as the shredded ACM 16 exitsthe shredding system 14. The delivery rate of the borax solution throughthe supply line 60 and the header 46 is regulated by the timed valve 62based on the weight measured by a weight sensor 68 of the ACM enteringthe shredder 14. Excess mineralizing agent 42 may be collected andtransported to the day tank 56 for reuse.

In accordance with another embodiment, the mineralizing agent comprisesan alkali metal hydroxide solution, an alkali metal silicate solution,an alkali metal borate, an alkaline earth borate solution, or mixturesthereof, having a concentration between about 8 to and including 12percent by weight.

The mineralizing agent 42 may be heated or maintained at a temperaturein the range of 120 degrees Fahrenheit and 160 degrees Fahrenheit. Theinterconnected mix tank 54, day tank 56, recirculation lines 60 andapplication header 46 are preferably heated, heat traced, or insulatedto preserve energy and to maintain the temperature of the mineralizingagent in the range of about 120 degrees Fahrenheit and 160 degreesFahrenheit.

The ACM 12 is delivered to the shredder 14 ideally at a rate determinedby the capacity of the system 10. The shredding system 14 may include ashredder, grinder, crusher, or metal detection system.

In addition, the shredder 14, housing and mixer 18, and transfermechanism 52, are operated at a vacuum in the range of 0.4 inches ofwater and 0.6 inches of water. In a preferred embodiment the encasedhousing is equipped with ductwork 70, blowers 72, and filters 74 tocapture emissions, particles, and dust.

In overview, the shredded ACM 17 that is treated with the mineralizingagent 42 is subsequently compacted 20, and the compacted ACM is brokenup into particles 30 that are spread 32 in the ACM mineralizing furnace24 for mineralization and then moved for cooling in an enclosed,atmosphere-controlled area, all of which is described above in greaterdetail. The cooled resultant mineralized material is packaged and movedto an area for further handling or disposal. The resultant mineralizedmaterial contains non-detectable concentrations of asbestos whenanalyzed using transmission electron microscopy, X-ray diffraction, andoptical microscopy techniques.

While the ACM 12 can be manually fed into the shredding system 14, amechanical apparatus can be used to deliver plastic bags that containthe ACM 12 to a hopper that delivers the plastic bags to the shreddingsystem 14, which shreds the ACM 12. A conveyor or other suitable meanstransports the shredded ACM treated with the mineralizing agent forfurther downstream mineralizing treatment. The hopper receives the ACMand transports the ACM by any number of commonly available transfermechanisms, such as by gravity, conveyer, or other means of conveyance.The shredder 14 may be of any suitable type to prepare the ACM forapplication of the mineralizing agent, with the preferred embodimentusing a slow speed rip-shear shredder. In an alternative embodiment, acrosscut shredder with capacity commensurate with the heater/furnace canbe used.

The various embodiments described above can be combined to providefurther embodiments. All of the U.S. patents, U.S. patent applicationpublications, U.S. patent applications, foreign patents, foreign patentapplications, and non-patent publications referred to in thisspecification and/or listed in the Application Data Sheet, areincorporated herein by reference, in their entirety. Aspects of theembodiments can be modified, if necessary to employ concepts of thevarious patents, applications, and publications to provide yet furtherembodiments.

These and other changes can be made to the embodiments in light of theabove-detailed description. In general, in the following claims, theterms used should not be construed to limit the claims to the specificembodiments disclosed in the specification and the claims, but should beconstrued to include all possible embodiments along with the full scopeof equivalents to which such claims are entitled. Accordingly, theclaims are not limited by the disclosure.

1. An apparatus for treating an asbestos containing material (ACM) witha mineralizing agent for the purpose of converting the asbestos into anessentially asbestos-free mineral that contains non-detectableconcentrations of asbestos when analyzed using transmission electronmicroscopy, X-ray diffraction, and optical microscopy techniques, theapparatus comprising: a shredding system structured to receive and shredthe ACM into shredded ACM in the shredding apparatus to increase thesurface area and to discharge the shredded ACM; and a delivery systemadapted to apply the mineralizing agent to the shredded ACM after it isdischarged and while the shredded ACM is falling through the air fromthe shredding apparatus.
 2. The apparatus of claim 1 wherein thedelivery system comprises a spray system adapted to spray themineralizing agent to the shredded ACM.
 3. The apparatus of claim 1,further comprising a device to weigh the amount of the shredded ACMbefore applying the mineralizing agent to the shredded ACM.
 4. Theapparatus of claim 3 wherein the delivery system is adapted to deliverthe mineralizing agent to the shredded ACM at a rate based upon theweighed amount of the shredded ACM.
 5. The apparatus of claim 1 whereinthe mineralizing agent delivery system is adapted to measure the rate atwhich the mineralizing agent is applied to the shredded ACM.
 6. Theapparatus of claim 5 wherein the mineralizing agent delivery system isadapted to deliver the mineralizing agent to the shredded ACM at a ratebased upon the rate at which the ACM is shredded.
 7. The apparatus ofclaim 1 wherein the delivery system further comprises a unit adapted toheat the mineralizing agent before applying the mineralizing agent tothe shredded ACM.
 8. A system for treating an asbestos containingmaterial (ACM) particles with a mineralizing agent to convert theasbestos within the ACM particles into essentially asbestos-freeminerals, the system comprising: a reduction unit structured to reducethe size of the ACM particles to form a reduced size ACM and todischarge the reduced size ACM into a housing; a treating unitstructured to treat the reduced size ACM with a mineralizing agent in aspray, mist, atomized, droplet, or other highly dispersed form after theshredded ACM is discharged and while the shredded ACM is falling throughthe housing to form a treated ACM; a compaction unit structured tocompress the treated ACM into a compressed ACM; a unit structured tobreak up the compressed ACM into broken-up particles; a unit structuredto spread the broken-up particles in a furnace; a heat source structuredto apply heat directly to the broken up particles to form heated brokenup particles; and an enclosed atmosphere-controlled cooling unitstructured to cool the heated broken up particles.
 9. The system ofclaim 8 wherein the reduction unit comprises a shredding system thatforms shredded ACM.
 10. The system of claim 9, further comprising a unitthat moves the heated broken up particles while hot on a floor of afurnace containing the heat source.
 11. The system of claim 9 whereinthe unit that treats the shredded ACM with the mineralizing agentfurther comprises a spray apparatus.
 12. The system of claim 11, furthercomprising a system that weighs the amount of the ACM to determine theweight of the weighed ACM before the mineralizing agent is applied tothe shredded ACM.
 13. The system of claim 12, further comprising asystem that controls the rate of applying an amount of the mineralizingagent to the shredded ACM based on the weight of the weighed ACM. 14.The system of claim 8 wherein the unit that treats the shredded ACM withthe mineralizing agent further comprises: a system to measure the rateat which the shredding system shreds the ACM into the shredded ACM; anda system that controls the rate of applying the mineralizing agent tothe shredded ACM based on the rate at which the shredding system shredsthe ACM.
 15. The system of claim 11, further comprising a unit thatheats the mineralizing agent before the mineralizing agent is applied tothe shredded ACM.
 16. The system of claim 8, further comprising a systemthat moves the heated broken up particles into an enclosed,atmosphere-controlled area where the heated broken up particles coolgradually.
 17. A device for treating an asbestos containing material(ACM) with a mineralizing agent for the purpose of converting theasbestos into an essentially asbestos-free mineral that containsnon-detectable concentrations of asbestos when analyzed usingtransmission electron microscopy, X-ray diffraction, and opticalmicroscopy techniques, the device comprising: a shredder structured toshred the ACM into shredded ACM and discharging the shredded ACM underpressure through a screen containing openings; and an apparatusstructured to spray the mineralizing agent over the shredded ACM afterit is discharged and while the shredded ACM is falling through the airfrom the shredding apparatus.
 18. The device of claim 17 wherein theshredder is structured to discharge the shredded ACM by propulsionthrough the screen that is structured to contain openings approximately2 inches in diameter.
 19. The device of claim 17 further comprising anassembly structured to collect excess mineralizing agent and return itto the apparatus structured to spray the mineralizing agent.
 20. Thedevice of claim 17, comprising a scale assembly structured to weigh theamount of ACM fed to the shredding system before applying themineralizing agent to the shredded ACM so that the mineralizing agent isapplied in amounts based on the weight of the ACM fed to the shredder.21. The device of claim 17, comprising means for heating themineralizing agent to a temperature in the range of about 120 degreesFahrenheit and about 160 degrees Fahrenheit before applying themineralizing agent to the shredded ACM.
 22. The device of claim 17,further comprising an assembly structured to compact the shredded ACMafter the mineralizing agent is applied, an assembly structured to breakthe compacted ACM into particles, an assembly structured to spread theACM particles in a furnace while heating the ACM particles in thefurnace, and an assembly to move the heated ACM particles into anenclosed, atmosphere-controlled container for cooling.